Oxidative treatment method of high-salt wastewater containing calcium chloride
A high-salt wastewater, oxidation treatment technology, applied in the direction of oxidation water/sewage treatment, water/sewage treatment, chemical instruments and methods, etc., can solve the problem of reducing the efficiency of mass transfer and heat transfer, unfavorable use of calcium chloride, and generation of secondary Secondary wastewater and other problems, to achieve the effect of low treatment cost, low organic matter content, and reduced treatment cost
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Embodiment 1
[0032] Add the wastewater from the production of epichlorohydrin to the oxidation reactor, add a homogeneous catalyst, raise the temperature and feed the oxidant, under the action of the homogeneous catalyst, the organic matter in the wastewater reacts with the oxidant and degrades into small molecular organic matter, small molecule The organic matter enters the fixed-bed reactor filled with solid catalyst along with the evaporated steam and oxidant, and the small molecular organic matter is completely oxidized into water and carbon dioxide in the fixed-bed reactor. The oxidized waste water is exchanged with the incoming water through the heat exchange device, heat recovery. The temperature, flow rate and residence time of the reaction are controlled, and the water is sampled for analysis after the reaction is completed. The wastewater in the oxidation reactor is continuous water inflow. As the reaction progresses, the CaCl in the reactor 2 After the concentration gradually r...
Embodiment 2
[0037] Wastewater treatment process is the same as embodiment 1.
[0038] The process parameters are:
[0039] CaCl in epichlorohydrin production wastewater 2 The content is 15.0wt.%, and the COD is 5000mg / L; after copper chloride is added to the wastewater produced by epichlorohydrin, Cu 2+The molar concentration in the epichlorohydrin production wastewater is 0.7mmol / L; the temperature in the oxidation reactor is 160°C, and the residence time is 5min; the secondary oxidation fixed-bed reactor is filled with porous solid catalyst Co / C, and the reaction temperature is 230°C, the residence time is 5min, the flow rate of wastewater is 150ml / min, and the oxidant is oxygen.
[0040] After testing, the removal rate of COD in the treated organic wastewater is 97.20%. CaCl 2 The recovery rate is 94.8%, and the solid salt is analyzed after drying, and its quality index is: CaCl 2 : 97.8wt.%; Cu 2+ : 2.0 μg / g; TOC: 5.1 μg / g.
Embodiment 3
[0042] Wastewater treatment process is the same as embodiment 1.
[0043] The process parameters are:
[0044] CaCl in epichlorohydrin production wastewater 2 The content is 15.0wt.%, and the COD is 5000mg / L; after adding ferric chloride to the wastewater produced by epichlorohydrin, Fe 3+ The molar concentration in the epichlorohydrin production wastewater is 0.8mmol / L; the temperature in the oxidation reactor is 170°C, and the residence time is 10min; the secondary oxidation fixed-bed reactor is filled with porous solid catalyst Co / C, and the reaction temperature is 240°C, the residence time is 3min, the flow rate of wastewater is 100ml / min, and the oxidant is oxygen.
[0045] After testing, the removal rate of COD in the treated organic wastewater is 98.2%, CaCl 2 The recovery rate is 95.1%, and the solid salt is analyzed after drying, and its quality index is: CaCl 2 : 94.8wt.%; Fe 3+ : 2.0 μg / g; TOC: 5.8 μg / g.
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